Organocatalysis

Résumé

In organic chemistry, organocatalysis is a form of catalysis in which the rate of a chemical reaction is increased by an organic catalyst. This "organocatalyst" consists of carbon, hydrogen, sulfur and other nonmetal elements found in organic compounds. Because of their similarity in composition and description, they are often mistaken as a misnomer for enzymes due to their comparable effects on reaction rates and forms of catalysis involved. Organocatalysts which display secondary amine functionality can be described as performing either enamine catalysis (by forming catalytic quantities of an active enamine nucleophile) or iminium catalysis (by forming catalytic quantities of an activated iminium electrophile). This mechanism is typical for covalent organocatalysis. Covalent binding of substrate normally requires high catalyst loading (for proline-catalysis typically 20–30 mol%). Noncovalent interactions such as hydrogen-bonding facilitates low catalyst loadings (down to 0.0

Source officielle

https://en.wikipedia.org/wiki/Organocatalysis

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Rising level of carbon dioxide (CO2) is a significant contributor to global warming and poses a major concern in modern society and environment. Anthropogenic activities such as fossil fuel combustion, cement production and deforestation are the primary causes of CO2 emissions. Creating sustainable pathways by converting abundantly available CO2 into fuel could help in mitigating the ever-growing global energy demand. Owing to the high intrinsic thermodynamic stability of CO2 molecule, the chemical reduction mechanism requires an appropriate catalyst system to reduce the high activation energy barrier. Additionally, the prospect of utilising CO2 as C1 synthon to convert the amines to afford value-added formamides is even more appealing. In the present dissertation, the development of efficient industrial friendly heterogeneous catalytic routes for CO2 fixation on amines by chemical reduction method to formamides, as well as their subsequent conversion to fuel, methanol under mild conditions are investigated. The first chapter describes an overview about the current trends in global climate change, about the challenges in CO2 capture and storage, the employment of CO2 as a source of carbon to synthesise industrially essential formamide products by catalytic reduction. Subsequently, the reduction pathway of formamides to afford methanol is also elucidated. Additionally, the prospect of using formic acid (a known CO2 and H2 carrier) to formylate amines and the consequent reduction to methanol is also given. The combination of these reactions presents a viable CO2 reduction system using amines. In the second chapter, N-formylation and N-methylation of amines using CO2 as the carbon source catalysed by palladium nanoparticles (Pd NPs) under mild conditions are discussed. The concluding results point out the high efficiency and high selectivity of Pd NPs in catalysing the amines to fix CO2 to afford formamides at room temperature. The Pd NPs exhibited excellent catalytic activity and selectivity on par with the reported catalysts. The overall selectivity and conversion of the products could be altered by adjusting the CO2 pressure, catalyst loading, temperature and solvent. The catalyst could be recycled for multiple reactions without significant loss of activity. The third chapter describes a âGeo-inspiredâ catalyst system with the use of an iron-rich natural mineral-Gibeon meteorite, as the catalyst for N-formylation and N-methylation of amines using CO2 as the carbon source at room temperature. Similar to the second chapter, the Gibeon meteorite exhibited excellent catalytic activity and selectivity on par with the reported catalysts. The overall selectivity and conversion could be altered by adjusting the CO2 pressure, catalyst loading, temperature and solvent. Comparative studies with the similar iron-containing alloys were also carried out. A plausible mechanism is proposed with the Gibeon meteoriteâs surface bound hydroxide ions. Moreover, the catalyst could be easily recovered and reused for multiple reactions as well without significant loss of activity. The fourth chapter encompasses the investigation of a metal-free catalytic system using polymerisable ionic liquid- (4-Vinylbenzyl)trimethylammonium chloride catalysed N-formylation and N-methylation of amines using CO2 as the carbon source under mild conditions. Similar to second and third chapters, the monomer and the polymer exhibited excellent catalytic activity (comparable

EPFL2018

Chargement

Synthesis of Cross-linked Ionic Poly(styrenes) and their Application as Catalysts for the Synthesis of Carbonates from CO2 and Epoxides

Felix Daniel Bobbink, Paul Joseph Dyson, Zhaofu Fei, Aswin Gopakumar, Antoine Philippe Van Muyden

A series of dicationic styrene-functionalized imidazolium-based salts, in which the two imidazolium rings are bridged by a functionalized spacer, are prepared. The salts are polymerized to afford cross-linked imidazolium-based ionic polystyrene materials, which, owing to the presence of the functionalized spaces, should be highly active organocatalysts for the cycloaddition of CO2 to epoxides to afford cyclic carbonates (CCE reaction). The catalytic activities of the polymers are evaluated in the CCE reaction. The most active catalyst incorporates a diol functionality and is active at 80 degrees C and a pressure of 4bar at a loading of 5mol%, which is comparable to the most active organocatalysts. Moreover, high yields can be obtained under atmospheric pressure upon increasing the temperature to 120 degrees C. Under harsher conditions, the catalyst is highly active at a loading one order of magnitude lower, highlighting the importance of benchmark conditions for the CCE reaction. Moreover, the polymer catalysts are advantageous because they can be used at low catalyst loadings, the carbonate product is easily isolated in pure form, and loss of activity of the recovered polymer catalyst is not observed during reuse.

Wiley-VCH Verlag2017

Chargement

Compact reactor for continuous multi-phase reactions

Martin Grasemann

The objective of this thesis is the development of a compact reactor for continuous three-phase reactions in single-pass configurations. The design is based on a bubble column reactor staged with layers of catalytic material. To make the reactor suitable for reactions with high adiabatic temperature rise such as highly exothermic hydrogenation reactions under solvent free conditions, work focuses on two different aspects of integrated reactor and catalyst design: Preparation and characterization of structured catalyst stages optimized for high intrinsic activity as well as for intense gas-liquid redistribution and mass transfer on each reactor stage Development of heat transfer equipment integrated in the staged bubble column for efficient, quasi continuous in-line removal of process heat. Chapter 3 is dedicated to the preparation and characterization of a structured catalyst for the use in a staged bubble column reactor. Sintered Metal Filters (SMF), a material consisting of metal fibers with a diameter of ~ 20 µm forming thin and highly porous sheets is chosen as support material. The fibers are coated with a 5wt% layer of ZnO grains, leaving the open structure of the SMF material intact. Monodispersed Pd nanoparticles as active phase are deposited on the ZnO surface layer with a total metal loading of 0.2wt%. The resulting Pd/ZnO/SMF catalyst shows high activity in the model hydrogenation reaction of 2-methyl-3-butyn-2-ol (MBY) to 2-methyl-3-butene-2-ol (MBE). Semi-batch autoclave hydrogenations show rates of up to 30 mol/molPds with target product (MBE) yields of up to 96.5%. Activity and selectivity of the Pd/ZnO/SMF catalyst are strongly influenced by Strong Metal Support Interaction (SMSI) between the ZnO support and the deposited Pd nanoparticles. XPS and XRD analysis show the formation of a PdZn alloy already under ambient conditions, decreasing the catalyst activity but, on the other hand, preventing strong catalyst deactivation. The formation of this alloy phase was observed under ambient conditions as well as low temperature reaction conditions, but can also be achieved by high temperature treatment of the catalyst in hydrogen atmosphere. The intrinsic kinetics of the MBY hydrogenation was studied in semi-batch experiments. First order towards hydrogen was found and a Langmuir-Hinshelwood kinetic model was developed, describing the experimental data reasonably well. Chapter 4 describes a compact heat exchange (HEX) element integrated in the SBCR. The cross flow heat exchanger design is based on vertical micro-slits of 0.3mm width, a breadth between 12mm and 40mm and 6mm length as reaction side channel geometry, ensuring a minimum of added reaction volume and small heat transfer distances. The single and two-phase heat transfer performance of the HEX element is studied considering the influence of gas and liquid superficial velocities as well as liquid properties. With one SMF layer placed at the HEX element entrance redispersing gas and liquid phase, heat transfer performance was observed to increase linearly with gas and liquid throughput. The maximum heat transfer performance per reaction volume was determined as ~ 0.5 MW/m3K, obtained for moderate gas and liquid superficial velocities. The hydrodynamics of a bubble column staged only with ZnO/SMF sheets show an narrow residence time distribution (RTD) and negligible backmixing through the catalyst layers. The RTD can be described accurately by a "tanks-in-series" model. The gas-liquid pressure drop through the SMF material is mainly governed by capillary effects and the gas velocity. A semi-empirical model is developed, combining both friction and surface tension effects and predicting the pressure drop through the SMF material with an accuracy of ±10%. In Chapter 5, the novel SBCR based on Pd/ZnO/SMF catalytic stages and the integrated micro-HEX elements are tested in the hydrogenation model reaction of MBY to MBE. The reaction in a loop setup comprising 5 HEX/catalyst stages is shown to be strongly influenced by external mass transfer, resulting in an observed catalyst effectiveness below 65%. Intense gas-liquid mass transfer in the SMF structure leads to high volumetric mass transfer coefficient in the staged bubble column of 1s-1 - 4s-1 and an observed reactor productivity of up to ~ 12000 kg/m3h. This signifies an increase of around two orders of magnitude compared to standard industrial semi-batch equipment. High catalyst densities in the reactor lead to high reactor productivity, but have a detrimental effect on product selectivity. The drop in product yield amounts up to 6% for high catalyst density, but can be decreased to only 0.5% if a 5mm distance ring is inserted between HEX stages to decrease the catalyst loading in the reactor.

EPFL2009

Chargement

Compact reactor for continuous multi-phase reactions

Martin Grasemann

EPFL2009

EPFL2018